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Synthesis, Characterization, and Gas Permeation Properties

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Silylation of Ethyl Cellulose<br />

1.034), which is probably due to its highest van der Waals volume.<br />

<strong>Gas</strong> <strong>Permeation</strong> <strong>Properties</strong>. The permeability coefficients of the<br />

membranes of polymers 1 <strong>and</strong> 2a–f to various gases measured at 25 °C are listed in<br />

Table 4, <strong>and</strong> their plot versus kinetic diameter of gases is shown in Figure 4. The gas<br />

permeability of the silylated derivatives was higher than that of ethyl cellulose, <strong>and</strong><br />

Table 4. <strong>Gas</strong> Permeability Coefficients (P) of Polymer Membranes at 25 o C<br />

polymer<br />

Table 3. Physical <strong>Properties</strong> of Polymers 1 <strong>and</strong> 2a–f<br />

polymer T0 a ( o C) υw b (cm 3 /mol) ρ c (g/cm 3 ) FFV d<br />

1 338 135.8 1.095 0.185<br />

2a 280 152.1 1.076 0.180<br />

2b 283 162.1 1.065 0.177<br />

2c 305 159.0 1.067 0.178<br />

2d 298 162.1 1.083 0.163<br />

2e 273 183.8 1.034 0.148<br />

2f 338 162.6 1.091 0.173<br />

a Onset temperature of weight loss observed from TGA measurement in air. b υw:<br />

van der Waals volume. c ρ: density. Determined by hydrostatic weighing. d FFV: fractional<br />

free volume. Estimated from membrane density.<br />

P (barrer) a<br />

He H2 O2 N2 CO2 CH4<br />

42<br />

PCO2/PN2 PCO2/PCH4<br />

1 53 76 18 5.0 110 12 22 9.2<br />

2a 98 160 45 14 250 35 18 7.1<br />

2b 81 130 42 13 230 33 18 7.0<br />

2c 82 130 40 13 230 31 18 7.4<br />

2d 67 100 27 8.0 150 18 19 8.3<br />

2e 65 98 31 10 150 25 15 6.0<br />

2f 58 86 23 7.0 130 15 19 8.7<br />

a 1 barrer = 1x10 -10 cm 3 (STP) cm cm -2 s -1 cmHg -1 .

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